CN113121782B - Polyurethane elastomer raw material, polyurethane elastomer and preparation method thereof - Google Patents

Polyurethane elastomer raw material, polyurethane elastomer and preparation method thereof Download PDF

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CN113121782B
CN113121782B CN201911396675.1A CN201911396675A CN113121782B CN 113121782 B CN113121782 B CN 113121782B CN 201911396675 A CN201911396675 A CN 201911396675A CN 113121782 B CN113121782 B CN 113121782B
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polyurethane elastomer
compound
membered saturated
substituted
temperature
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CN113121782A (en
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刘小孔
李泽权
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Jilin University
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Jilin University
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/08Processes
    • C08G18/10Prepolymer processes involving reaction of isocyanates or isothiocyanates with compounds having active hydrogen in a first reaction step
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40High-molecular-weight compounds
    • C08G18/48Polyethers
    • C08G18/4854Polyethers containing oxyalkylene groups having four carbon atoms in the alkylene group
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/65Low-molecular-weight compounds having active hydrogen with high-molecular-weight compounds having active hydrogen
    • C08G18/66Compounds of groups C08G18/42, C08G18/48, or C08G18/52
    • C08G18/6666Compounds of group C08G18/48 or C08G18/52
    • C08G18/667Compounds of group C08G18/48 or C08G18/52 with compounds of group C08G18/32 or polyamines of C08G18/38
    • C08G18/6681Compounds of group C08G18/48 or C08G18/52 with compounds of group C08G18/32 or polyamines of C08G18/38 with compounds of group C08G18/32 or C08G18/3271 and/or polyamines of C08G18/38
    • C08G18/6685Compounds of group C08G18/48 or C08G18/52 with compounds of group C08G18/32 or polyamines of C08G18/38 with compounds of group C08G18/32 or C08G18/3271 and/or polyamines of C08G18/38 with compounds of group C08G18/3225 or polyamines of C08G18/38
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L75/00Compositions of polyureas or polyurethanes; Compositions of derivatives of such polymers
    • C08L75/04Polyurethanes
    • C08L75/08Polyurethanes from polyethers

Abstract

The invention discloses a polyurethane elastomer raw material, a polyurethane elastomer and a preparation method thereof. The structure of the polyurethane elastomer is shown as a formula I. The polyurethane elastomer has ultrahigh strength and toughness, excellent thermal stability and tear resistance, and good application and popularization prospects.

Description

Polyurethane elastomer raw material, polyurethane elastomer and preparation method thereof
Technical Field
The invention relates to a polyurethane elastomer raw material, a polyurethane elastomer and a preparation method thereof.
Background
In recent years, self-repairing polyurethane materials based on reversible covalent bonds have been well developed, but most of various self-repairing polyurethane materials have poor mechanical properties (such as strength and toughness) and greatly limit the application of the self-repairing polyurethane materials. Chinese patent application CN107236106A utilizes the reaction of an aromatic hydroxyl-terminated chain extender containing acylhydrazone bond and an isocyanate-terminated polyurethane prepolymer to prepare the self-repairing polyurethane, and the tensile strength of the self-repairing polyurethane material is maximally improved to 2.75MPa, and the elongation at break is maximally improved to 495.37%. However, the method can not meet the application occasions with high requirements on the mechanical properties of the self-repairing polyurethane, and the mechanical properties of the self-repairing polyurethane still have a large improvement space.
Disclosure of Invention
The invention aims to overcome the defect of poor mechanical properties such as strength, toughness and the like of a self-repairing polyurethane material in the prior art, and provides a polyurethane elastomer raw material, a polyurethane elastomer and a preparation method thereof. The polyurethane elastomer has ultrahigh strength and toughness, and has excellent thermal stability and tear resistance.
In order to achieve the above purpose, the present invention adopts the following technical scheme:
a polyurethane elastomer has a structure shown in a formula I:
wherein R is a Is thatWherein, the ring Q is 3-10 membered saturated carbocyclyl or R substituted 3-10 membered saturated carbocyclyl; r is R a1 Is connected with 1-bit N, R a3 Is connected with the 2-bit N; r is R a1 、R a2 And R is a3 Each independently is a bond, - (CH) 2 ) 1~4 -, 3-to 10-membered saturated carbocyclyl, R-substituted 3-to 10-membered saturated carbocyclyl, 6-to 18-membered aryl or R-substituted 6-to 18-membered aryl; and R is a1 、R a2 And R is a3 At most one of which is a 6-18 membered aryl or R-substituted 6-18 membered aryl;
alternatively, R a Is- (CH) 2 ) 2~10 -or R-substituted- (CH) 2 ) 2~10 -;
The R is one or more, and each R is independently C 1-4 Alkyl or halo C 1-4 An alkyl group;
R b removing residual structures of hydroxyl hydrogen at two ends of polyether glycol or polyester glycol;
R c is- [ (CH) 2 ) i -(NHC(=O)) j -(CH 2 ) k ] x -wherein i, j, k and x are each independently 0, 1 or 2; when i, j and k are simultaneously 0, and/or x is 0, R c Is a connecting key;
m=20~40;
the molecular weight distribution index of the polyurethane elastomer is 1-2.5.
In the present invention, the ring Q is preferably a 5-to 8-membered saturated carbocyclyl group or an R-substituted 5-to 8-membered saturated carbocyclyl group; the ring Q is more preferably a 6-membered saturated carbocyclyl or an R-substituted 6-membered saturated carbocyclyl; the R-substituted 6-membered saturated carbocyclyl is preferably C 1-4 Alkyl substituted 6 membered saturated carbocyclyl, more preferably methyl substituted 6 membered saturated carbocyclyl.
In the present inventionPreferably, the R a1 、R a2 And R is a3 Respectively are a connecting bond, -CH 2 -and a connection key. Preferably, said R a1 、R a2 And R is a3 Respectively are a connecting bond, -CH 2 -and 6-membered saturated carbocyclyl. Preferably, said R a1 、R a2 And R is a3 Respectively are a connecting bond, -CH 2 -and phenyl.
In the present invention, R a Preferably- (CH) 2 ) 6~8 -or R-substituted- (CH) 2 ) 6~8 -, more preferably- (CH) 2 ) 6 -。
In the present invention, R is more preferably a Is that
More preferably
In the present invention, preferably, the polyether glycol or polyester glycol is selected from polytetrahydrofuran glycol, polyethylene adipate glycol, polyethylene glycol adipate, 1, 4-butanediol adipate glycol and polyethylene glycol. The polyether glycol or polyester glycol preferably has a number average molecular weight of 2000 to 3000.
In the present invention, R is more preferably b Is thatn=28~42。
In the present invention, preferably, R c Is a bond, - (CH) 2 ) 4 -or-CH 2 -NHC(=O)-CH 2 -。
In a preferred embodiment of the present invention, the polyurethane elastomer has the structural formula shown in formula I-1:
wherein m is 38 and n is 28; the polyurethane elastomer has a molecular weight distribution index (PDI) of 1.66.
In a preferred embodiment of the present invention, the polyurethane elastomer has the structural formula shown in formula I-2:
wherein m is 35, n is 28; the polyurethane elastomer has a molecular weight distribution index (PDI) of 1.86.
In a preferred embodiment of the present invention, the polyurethane elastomer has the structural formula shown in formula I-3:
wherein m is 28 and n is 28; the molecular weight distribution index (PDI) of the polyurethane elastomer was 2.23.
In a preferred embodiment of the present invention, the polyurethane elastomer has the structural formula shown in formula I-4:
wherein m is 22 and n is 28; the polyurethane elastomer has a molecular weight distribution index (PDI) of 1.96.
The invention also provides a preparation method of the polyurethane elastomer, which comprises the following steps:
(1) In a solvent, under the protection of gas, under the temperature of 60-80 ℃, under the action of a catalyst, carrying out a prepolymerization reaction on the compound A and the compound B to obtain a prepolymer;
(2) In a solvent, under the protection of gas, carrying out polymerization reaction on the prepolymer obtained in the step (1) and a compound C at the temperature of 30-50 ℃ to obtain a polyurethane elastomer shown in a formula I;
wherein R is a 、R b And R is c And m are as defined above; the mol ratio of the compound A to the compound B to the compound C is 2 (0.9-1.1) and 0.9-1.1.
In the present invention, the molar ratio of the compound A, the compound B and the compound C is preferably 2:1:1.
In a preferred embodiment of the present invention, the compound A is(isophorone diisocyanate), said compound B is +>(polytetrahydrofuran, n=28), said compound C is +.>(adipic acid dihydrazide).
In a preferred embodiment of the present invention, the compound A is(dicyclohexylmethane diisocyanate), said compound B being +.>(polytetrahydrofuran, n=28), said compound C is +.>(adipic acid dihydrazide).
In a preferred embodiment of the present invention, the compound A is(Isofluorenone di)Isocyanate), said compound B being +.>(polytetrahydrofuran, n=28), said compound C is +.>(oxalic acid dihydrazide).
In a preferred embodiment of the present invention, the compound A is(hexamethylene diisocyanate), said compound B being +.>(polytetrahydrofuran, n=28), said compound C is +.>(adipic acid dihydrazide).
In the present invention, the solvent in step (1) or step (2) may be a solvent conventionally used in the art, preferably a polar organic solvent such as one or more of N-methyl-2-pyrrolidone, N-dimethylformamide, N-dimethylacetamide (DMAc) and dimethylsulfoxide. The solvent is preferably N, N-dimethylacetamide (DMAc). The solvents described in step (1) or step (2) are the same or different.
In the present invention, in step (1) or step (2), the gas is preferably nitrogen.
In step (1) of the present invention, the catalyst may be an organotin catalyst or a tertiary amine catalyst conventional in such reactions in the art, preferably dibutyltin dilaurate (DBTDL), stannous octoate, triethylenediamine, bis (dimethylaminoethyl) ether or N, N-dimethylcyclohexylamine. The catalyst may be used in an amount conventional for such reactions, the mass ratio of the catalyst to the compound A being preferably 1: (100-500). For example, when the compound A is isophorone diisocyanate and the catalyst is dibutyltin dilaurate, the mass ratio of the two is preferably 1:111.
In the present invention, in the step (1), the time of the prepolymerization may be 2 to 5 hours, preferably 3 hours.
In the present invention, in the step (1), the temperature of the prepolymerization is preferably 70 ℃.
In the present invention, the compound B is preferably subjected to a water removal treatment prior to the step (1). The water removal treatment may be carried out by a method conventional in the art, preferably by stirring the compound B at 110℃under vacuum for 1 hour.
In the present invention, in the step (2), the temperature of the polymerization reaction is preferably 40 ℃.
In the present invention, in the step (2), the polymerization time may be 10 to 20 hours, preferably 15 hours.
In the present invention, step (2) is preferably: after the prepolymerization reaction in the step (1) is finished, the temperature of the system is cooled to 30-50 ℃, and a solution of the compound C is directly added into the system to carry out polymerization reaction.
In the present invention, it is preferable to carry out the post-treatment after the polymerization reaction in the step (2) is completed. The post-treatment may be carried out by a method conventional in the art, and preferably, the reaction solution after completion of the polymerization reaction is heated to volatilize the solvent, followed by vacuum drying. The temperature of the heating may be conventionally selected according to the nature of the solvent, preferably 80 ℃. The heating time can be determined according to the solvent volatilization condition, and is preferably 12h. The temperature of the drying may be conventionally selected according to the nature of the solvent, and is preferably 80 ℃. The drying time can be determined according to the actual drying condition, and is preferably 24 hours.
The invention also provides a polyurethane elastomer, which is prepared by the preparation method.
The invention provides a polyurethane elastomer raw material, which comprises a compound A, a compound B and a compound C, wherein,
the compound A is OCN-R a -NCO,
The compound B is HO-R b -OH,
The compound C is
Wherein R is a 、R b And R is c Is as defined above; the molar ratio of the compound A to the compound B to the compound C is 2 (0.9-1.1): (0.9-1.1), preferably 2:1:1.
On the basis of conforming to the common knowledge in the field, the above preferred conditions can be arbitrarily combined to obtain the preferred examples of the invention.
The reagents and materials used in the present invention are commercially available.
The invention has the positive progress effects that: the invention provides a polyurethane elastomer shown in a formula I, which has the advantages of ultrahigh strength and toughness (the tensile strength is more than 60MPa, even up to 80MPa, the elongation at break is more than 1400%, even up to 1706%), excellent tear resistance and thermal stability, and good application and popularization prospects.
Drawings
FIGS. 1 to 6 are the tensile curves of polyurethane elastomer samples of examples 1 to 4 and comparative examples 1 to 2, respectively, according to the present invention.
FIG. 7 is a graph showing the cyclic stretching curves of polyurethane elastomer samples of example 1 of the present invention at various waiting times.
FIG. 8 is a graph of hysteresis area and residual strain for various wait times for polyurethane elastomer samples of example 1 of the present invention.
FIG. 9 is a plot of the tensile curve of the polyurethane elastomer samples of example 1 of the present invention with and without notches.
FIG. 10 is a tensile curve of a polyurethane elastomer sample of example 1 of the present invention repaired at 100℃for various times.
FIG. 11 is a plot showing the tensile curve of a polyurethane elastomer sample of example 1 of the present invention repaired for 36h at various temperatures.
FIG. 12 is a plot of storage modulus versus loss modulus as a function of temperature for polyurethane elastomer samples of example 1 of the present invention.
FIG. 13 is a graph showing the change in loss tangent with temperature of a polyurethane elastomer sample of example 1 of the present invention.
FIG. 14 is a thermal weight loss curve of a polyurethane elastomer sample of example 1 of the present invention.
Fig. 15 is a wide angle X-ray diffraction pattern of a polyurethane elastomer sample of example 1 of the present invention.
FIG. 16 is a small angle X-ray diffraction pattern of a polyurethane elastomer sample of example 1 of the present invention.
FIG. 17 is an ultraviolet spectrum of a polyurethane elastomer sample of example 1 of the present invention.
FIGS. 18 to 23 are nuclear magnetic patterns of polyurethane elastomer samples of examples 1 to 4 and comparative examples 1 to 2, respectively, according to the present invention.
Detailed Description
The invention is further illustrated by means of the following examples, which are not intended to limit the scope of the invention. The experimental methods, in which specific conditions are not noted in the following examples, were selected according to conventional methods and conditions, or according to the commercial specifications.
Example 1
(1) Adding 10g of polytetrahydrofuran (PTMEG, mn=2000, n=28) into a three-port bottle provided with a stirrer and a vacuum pumping device, adjusting the temperature value to 110 ℃, stirring and vacuumizing for 1h under vacuum, reducing the temperature to 70 ℃ after vacuumizing is finished, dissolving 2.22g of isophorone diisocyanate (IP) and 0.02g of dibutyltin dilaurate (DBTDL) into 5ml of N, N-dimethylacetamide (DMAc), adding into the three-port bottle, reacting for 3h under the protection of nitrogen, and finally reducing the temperature to 40 ℃;
(2) Dissolving 0.86g of adipic Acid Dihydrazide (AD) into 50mL of N, N-dimethylacetamide at 100 ℃, rapidly adding the dissolved adipic acid dihydrazide solution into a three-necked flask by using a syringe, and reacting for 15h under the protection of nitrogen;
(3) Pouring the reaction solution into a glass culture dish, heating at 80 ℃ for 12 hours to volatilize the solvent, then placing the culture dish with the sample into a vacuum oven at 80 ℃, and vacuum drying for 24 hours to obtain the polyurethane elastomer, wherein the structure of the polyurethane elastomer is shown as a formula I-1.
Example 2
(1) Adding 10g of polytetrahydrofuran (PTMEG, mn=2000) into a three-port bottle provided with a stirrer and a vacuum pumping device, adjusting the temperature value to 110 ℃, stirring and vacuumizing for 1h under vacuum conditions, reducing the temperature to 70 ℃ after vacuumizing is finished, dissolving 2.62g of dicyclohexylmethane diisocyanate and 0.02g of dibutyltin dilaurate (DBTDL) into 5mL of N, N-dimethylacetamide (DMAc), adding into the three-port bottle, reacting for 3h under the protection of nitrogen, and finally reducing the temperature to 40 ℃;
(2) Dissolving 0.86g of adipic Acid Dihydrazide (AD) into 50mL of N, N-dimethylacetamide at 100 ℃, rapidly adding the dissolved adipic acid dihydrazide solution into a three-necked flask by using a syringe, and reacting for 15h under the protection of nitrogen;
(3) Pouring the reaction solution into a glass culture dish, heating at 80 ℃ for 12 hours to volatilize the solvent, then placing the culture dish with the sample into a vacuum oven at 80 ℃, and vacuum drying for 24 hours to obtain the polyurethane elastomer, wherein the structure of the polyurethane elastomer is shown as a formula I-2.
Example 3
(1) Adding 10g of polytetrahydrofuran (PTMEG, mn=2000) into a three-necked flask equipped with a stirrer and a vacuum pumping device, adjusting the temperature value to 110 ℃, stirring and vacuumizing for 1h under vacuum, after vacuumizing, reducing the temperature to 70 ℃, dissolving 2.22g of isophorone diisocyanate (IP) and 0.02g of dibutyltin dilaurate (DBTDL) into 5mL of N, N-dimethylacetamide (DMAc), adding into the three-necked flask, reacting for 3h under the protection of nitrogen, and finally reducing the temperature to 40 ℃;
(2) Dissolving 0.59g of oxalic acid dihydrazide in 70mL of N, N-dimethylacetamide at 130 ℃, rapidly adding the dissolved adipic acid dihydrazide solution into a three-mouth bottle by using a syringe, and reacting for 15h under the protection of nitrogen;
(3) Pouring the reaction solution into a glass culture dish, heating at 80 ℃ for 12 hours to volatilize the solvent, then placing the culture dish with the sample into a vacuum oven at 80 ℃, and vacuum drying for 24 hours to obtain the polyurethane elastomer, wherein the structure of the polyurethane elastomer is shown as a formula I-3.
Example 4
The procedure and conditions were the same as in example 1 except that 1.68g of hexamethylene diisocyanate was used in place of 2.22g of isophorone diisocyanate (IP) in example 1, and the structure of the resulting polyurethane elastomer was shown in formula I-4.
Comparative example 1
The procedure and conditions were otherwise identical to example 1 except that 1.74g of toluene 2, 4-diisocyanate (TDI) was used in place of 2.22g of isophorone diisocyanate (IP) in example 1, and the resulting polyurethane elastomer had the structure shown in formula II.
Comparative example 2
The procedure and conditions were the same as in example 1 except that 0.3g of ethylenediamine was used instead of 0.86g of Adipic Dihydrazide (AD) in example 1, and the structure of the resulting polyurethane elastomer was shown in formula III.
Effect example 1: structural characterization
1. Nuclear magnetic characterization
The polyurethane elastomers prepared in examples 1 to 4 and comparative examples 1 to 2 were subjected to nuclear magnetic characterization, specifically, 10mg of the sample was dissolved in 0.5mL of anhydrous deuterated chloroform on a Bruker 500M nuclear magnetic resonanceProceed H 1 The results of the test are shown in FIGS. 18 to 23.
2. Molecular weight and molecular weight distribution index (PDI)
The polyurethane elastomers obtained in examples 1 to 4 and comparative examples 1 to 2 were measured by using a Waters 2410 Gel Permeation Chromatography (GPC) method, and the sample concentration was about 2 to 3mg/mL, and the sample loading amount was 60 μl, using tetrahydrofuran as a mobile phase, measured at a flow rate of 1 mL/min. The polymerization degree m (calculated from the number average molecular weight measured) and PDI of each sample are shown in Table 1.
TABLE 1
Sample of Example 1 Example 2 Example 3 Example 4 Comparative example 1 Comparative example 2
m 38 35 28 22 11 18
n 28 28 28 28 28 28
PDI 1.66 1.86 2.23 1.96 1.85 2.53
Effect example 2: infrared test
The polyurethane elastomers prepared in examples 1 to 4 and comparative examples 1 to 2 were subjected to infrared test.
The testing method comprises the following steps: 7mg of the sample was dissolved in tetrahydrofuran and film was formed on a silicon wafer for testing.
Test instrument: infrared spectrometer VERTEX 80V (Brucker)
Infrared carbonyl removal of samples (1800-1600 cm) on Origin 7.5 -1 ) The peaks were separated, and the degree of hydrogen bonding was calculated from the assignment of the groups represented by each peak and the area ratio, and the results are shown in table 2. It can be seen that the degree of hydrogen bonding of the polyurethane elastomers of examples 1 to 4 of the present invention is 50% or more, even as high as 79.8%, far higher than that of the comparative example.
TABLE 2
Effect example 2: mechanical property test
1. Tensile test
The polyurethane elastomers prepared in examples 1 to 4 and comparative examples 1 to 2 were subjected to a tensile TEST at a tensile rate of 50mm/min in a 410R250 tensiometer (TEST RESOURCES inc., USA) at an effective area of 12mm×20mm×0.8mm, at room temperature, and at least 5 parallel samples were taken for each sample, and an average was taken. The tensile curves of the samples are shown in FIGS. 1 to 6, and the tensile strength and elongation at break are shown in Table 3.
TABLE 3 Table 3
As can be seen from Table 3, the polyurethane elastomers of examples 1 to 4 all had tensile strengths of 60MPa or more and elongation at break of 1400% or more, while having higher strengths and toughness. Comparative examples 1 and 2 have a low tensile strength although the elongation at break is high.
2. Rebound resilience test
The dumbbell-shaped sample (effective area 12mm×20mm×0.8 mm) of the polyurethane elastomer prepared in example 1 was prepared, and according to the method of the tensile test described above, the sample was first loaded to 400%, then unloaded, and the same loading and unloading were repeated for different times (1 min, 5min, 15min, 30min, 60min, 120min and 180 min), and the cyclic stretching curves of the sample were obtained as shown in fig. 7, and the hysteresis areas and residual strain curves corresponding to different waiting times were as shown in fig. 8. It can be seen that the sample has good rebound resilience, and when the sample is stretched for 400%, the hysteresis area of the sample is recovered to 93% of that of the original sample, and the residual strain is recovered to 12%.
3. Fracture energy test
The polyurethane elastomer prepared in example 1 was prepared into two rectangular samples (16 mm. Times.5 mm. Times.0.6 mm), and a 1mm notch was cut in the middle of one sample with a scalpel, and the other sample was not treated. The sample was clamped in the tensiometer, the distance between the upper and lower clamping plates was 10mm, the stretching speed was 3mm/min, the test temperature was room temperature, and a stretching curve was obtained by performing a stretching test, as shown in fig. 9. The breaking energy G is calculated according to the following formula c =221.4KJ/m 2 It can be seen that the sample has very good tear resistance.
Wherein c represents the length of the notch, lambda c Represents the fracture strain of the unnotched sample, w represents the strain-strain curve obtained by integrating the stress curve of the unnotched sample up to lambda c The calculated strain energy.
Effect example 3: repair Performance test
The polyurethane elastomer prepared in example 1 was prepared into a rectangular sample (40 mm. Times.20 mm. Times.0.8 mm), and a incision was made in the middle with a scalpel, and the sample was put into an oven at a certain temperature for repair; the repaired sample was cut into a dumbbell shape (effective area 12 mm. Times.2 mm. Times.0.8 mm) with the incision in the middle, and a tensile curve was obtained in accordance with the method of the tensile test in effect example 2. FIG. 10 shows the tensile curves of samples repaired at 100deg.C for different times (original, 6h, 12h, 24h and 36 h) and FIG. 11 shows the tensile curves of samples repaired at different temperatures (original, 70 ℃, 80 ℃, 90 ℃ and 100 ℃) for 36 h. Stress and strain repair efficiencies of samples at 100 ℃ for different times and at different temperatures for 36h are shown in table 4.
TABLE 4 Table 4
It can be seen that the repair efficiency of the sample was gradually increased with the increase of the repair time when the repair temperature of the sample was 100 c, and the mechanical properties of the sample were almost completely recovered when the sample was repaired for 36 hours. When the sample is repaired for 36h at different temperatures, the repair efficiency is gradually improved along with the increase of the repair temperature.
Effect example 4: thermal performance testing
1. Dynamic mechanical thermal analysis (DMA)
The polyurethane elastomer prepared in example 1 was prepared into rectangular samples (50 mm. Times.5 mm. Times.0.6 mm) and tested on an instrument TAQ800 at a temperature ranging from-100℃to 150℃and a heating rate of 5℃per minute. Fig. 12 is a plot of storage modulus versus loss modulus for a sample as a function of temperature, and it can be seen that both storage modulus and loss modulus decrease as the temperature of the sample increases. FIG. 13 shows the change in loss tangent with temperature for a sample having a soft segment Tg of-66℃and a hard segment Tg of 77 ℃.
2. Thermogravimetric analysis test
10g of the polyurethane elastomer prepared in example 1 was subjected to thermogravimetric analysis on a TAQ500 at a test temperature ranging from 25 to 800℃and a heating rate of 10℃per minute, and tested under an air atmosphere. FIG. 14 is a graph of thermal weight loss of a sample, showing that the sample has high thermal stability and an initial decomposition temperature of 250℃or higher.
Effect example 5: microstructure characterization
1. Wide angle X-ray diffraction (XRD)
The polyurethane elastomer prepared in example 1 was prepared into a rectangular sample (20 mm. Times.20 mm. Times.0.8 mm) and tested on a D/MAX2550 instrument, and the results are shown in FIG. 15. As can be seen from fig. 15, the sample was amorphous without crystallization.
2. Small angle X-ray diffraction (SAXS)
The polyurethane elastomer prepared in example 1 was prepared into rectangular samples (10 mm. Times.5 mm. Times.0.5 mm) and tested on a SAXSess mc2 instrument, the results of which are shown in FIG. 16. As can be seen from fig. 16, a strong scattering peak was observed at q=0.68 nm, demonstrating that microphase separation of the sample occurred.
Effect example 6: ultraviolet testing
A sample of the polyurethane elastomer prepared in example 1, 0.6mm, was subjected to UV testing using a UV spectrophotometer UV-2700 (SHIMADZU) according to conventional methods in the art, and the results are shown in FIG. 17. The sample has a light transmittance of 90% at 550nm and exhibits good transparency.

Claims (15)

1. A polyurethane elastomer is characterized in that the structure is shown as a formula I:
wherein,
R a is thatWherein, the ring Q is 5-8 membered saturated carbocyclyl or R substituted 5-8 membered saturated carbocyclyl; r is R a1 Is connected with 1-bit N, R a3 Is connected with the 2-bit N;
the R is a1 、R a2 And R is a3 Respectively are a connecting bond, -CH 2 -and a connecting key; alternatively, the R a1 、R a2 And R is a3 Respectively are a connecting bond, -CH 2 -and 6 membered saturated carbocyclyl;
alternatively, R a Is- (CH) 2 ) 2~10 -or R-substituted- (CH) 2 ) 2~10 -;
The R is one or more, and each R is independently C 1-4 Alkyl or halo C 1-4 An alkyl group;
R b removing residual structures of hydroxyl hydrogen at two ends of polyether glycol or polyester glycol; the number average molecular weight of the polyether glycol or the polyester glycol is 2000-3000;
R c is- [ (CH) 2 ) i -(NHC(=O)) j -(CH 2 ) k ] x -wherein j = 0, i, k and x are each independently 1 or 2;
m=20~40;
the molecular weight distribution index of the polyurethane elastomer is 1-2.5.
2. The polyurethane elastomer of claim 1, wherein the ring Q is a 6 membered saturated carbocyclyl or an R-substituted 6 membered saturated carbocyclyl.
3. The polyurethane elastomer of claim 2, wherein the R-substituted 6-membered saturated carbocyclyl is C 1-4 Alkyl substituted 6 membered saturated carbocyclyl.
4. The polyurethane elastomer of claim 2, wherein the R-substituted 6-membered saturated carbocyclyl is a methyl-substituted 6-membered saturated carbocyclyl.
5. The polyurethane elastomer of claim 1, wherein R a Is- (CH) 2 ) 6~8 -or R-substituted- (CH) 2 ) 6~8 -;
Alternatively, R a Is that
6. The polyurethane elastomer of claim 5, wherein R a Is- (CH) 2 ) 6 -。
7. The polyurethane elastomer of claim 1, wherein the polyether glycol or polyester glycol is selected from the group consisting of polytetrahydrofuran glycol, polyethylene adipate glycol, polyethylene glycol adipate, 1, 4-butanediol polyadipate glycol, and polyethylene glycol;
and/or R c Is a bond or- (CH) 2 ) 4 -。
8. The polyurethane elastomer of claim 1,
the structural formula of the polyurethane elastomer is shown as formula I-1:
wherein m is 38 and n is 28; the polyurethane elastomer has a molecular weight distribution index (PDI) of 1.66;
alternatively, the structural formula of the polyurethane elastomer is shown as formula I-2:
wherein m is 35, n is 28; the polyurethane elastomer has a molecular weight distribution index (PDI) of 1.86;
alternatively, the structural formula of the polyurethane elastomer is shown as formula I-3:
wherein m is 28 and n is 28; the polyurethane elastomer has a molecular weight distribution index (PDI) of 2.23;
alternatively, the structural formula of the polyurethane elastomer is shown as formula I-4:
wherein m is 22 and n is 28; the polyurethane elastomer has a molecular weight distribution index (PDI) of 1.96.
9. A process for the preparation of a polyurethane elastomer as claimed in any one of claims 1 to 8, characterized in that it comprises the following steps:
(1) In a solvent, under the protection of gas, under the temperature of 60-80 ℃, under the action of a catalyst, carrying out a prepolymerization reaction on the compound A and the compound B to obtain a prepolymer;
(2) In a solvent, under the protection of gas, carrying out polymerization reaction on the prepolymer obtained in the step (1) and a compound C at the temperature of 30-50 ℃ to obtain a polyurethane elastomer shown in a formula I;
wherein R is a 、R b And R is c And m is as defined in any one of claims 1 to 7; by a means ofThe mol ratio of the compound A to the compound B to the compound C is 2 (0.9-1.1) to 0.9-1.1.
10. The method for producing a polyurethane elastomer according to claim 9, wherein the molar ratio of the compound a, the compound B and the compound C is 2:2:1.
11. A process for preparing a polyurethane elastomer as claimed in claim 9, wherein,
the compound A isThe compound B is->n=28, said compound C is +.>
Or, the compound A isThe compound B isn=28, said compound C is +.>
Or, the compound A isThe compound B is->n=28, said compound C is +.>
Or, the compound A isThe compound B is->n=28, said compound C is +.>
12. A process for preparing a polyurethane elastomer as claimed in claim 9, wherein,
in the step (1) or the step (2), the solvent is a polar organic solvent;
and/or in the step (1) or the step (2), the gas is nitrogen;
and/or in the step (1), the catalyst is an organotin catalyst or a tertiary amine catalyst;
and/or, in the step (1), the time of the prepolymerization reaction is 2-5 h;
and/or, in the step (1), the temperature of the prepolymerization reaction is 70 ℃;
and/or, prior to step (1), subjecting said compound B to a water removal treatment;
and/or, in the step (2), the temperature of the polymerization reaction is 40 ℃;
and/or, in the step (2), the time of the polymerization reaction is 10-20 h;
and/or, the step (2) is as follows: after the prepolymerization reaction in the step (1) is finished, cooling the temperature of the system to 30-50 ℃, and directly adding a solution of a compound C into the system to perform polymerization reaction;
and/or, after the polymerization reaction in the step (2) is finished, carrying out post-treatment.
13. A process for preparing a polyurethane elastomer as claimed in claim 12, wherein,
in the step (1) or the step (2), the solvent is one or more of N-methyl-2-pyrrolidone, N-dimethylformamide, N-dimethylacetamide and dimethyl sulfoxide;
and/or in step (1), the catalyst is dibutyltin dilaurate, stannous octoate, triethylenediamine, bis (dimethylaminoethyl) ether, or N, N-dimethylcyclohexylamine;
and/or the mass ratio of the catalyst to the compound A is 1: (100-500);
and/or, in the step (1), the time of the prepolymerization reaction is 3h;
and/or, the water removal treatment is to stir the compound B at 110 ℃ under vacuum for 1h;
and/or, in the step (2), the time of the polymerization reaction is 15h;
and/or, the post-treatment is to heat and volatilize the solvent from the reaction liquid after the polymerization reaction is finished, and then vacuum drying is carried out.
14. A process for preparing a polyurethane elastomer as claimed in claim 13, wherein,
in the step (1) or the step (2), the solvent is N, N-dimethylacetamide;
and/or, the temperature of the heating is 80 ℃;
and/or, the heating time is 12h;
and/or, the drying temperature is 80 ℃;
and/or, the drying time is 24 hours.
15. Polyurethane elastomer, characterized in that it is produced by the production process according to any one of claims 9 to 14.
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Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1248181A (en) * 1969-01-22 1971-09-29 Bayer Ag Segmented polyurethane elastomers
US4286014A (en) * 1978-01-31 1981-08-25 Toray Industries, Incorporated Composite sheet material
CN109265636A (en) * 2018-08-10 2019-01-25 四川大学 Novel high-performance THERMALLY REVERSIBLE COVALENT polymer based on amide groups urea bond and preparation method thereof

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1248181A (en) * 1969-01-22 1971-09-29 Bayer Ag Segmented polyurethane elastomers
US4286014A (en) * 1978-01-31 1981-08-25 Toray Industries, Incorporated Composite sheet material
CN109265636A (en) * 2018-08-10 2019-01-25 四川大学 Novel high-performance THERMALLY REVERSIBLE COVALENT polymer based on amide groups urea bond and preparation method thereof

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